Property | Value | Unit | Source |
---|---|---|---|
ω | 0.2620 | KDB | |
PAff | [848.50; 848.80] | kJ/mol |
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PAff | 848.80 | kJ/mol | NIST |
PAff | 848.50 | kJ/mol | NIST |
BasG | [819.20; 819.60] | kJ/mol |
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BasG | 819.60 | kJ/mol | NIST |
BasG | 819.20 | kJ/mol | NIST |
ΔcH°liquid | -4795.50 ± 1.30 | kJ/mol | NIST |
EA | 0.17 ± 0.03 | eV | NIST |
ΔfG° | 226.10 | kJ/mol | Joback Calculated Property |
ΔfH°gas | 161.20 ± 2.30 | kJ/mol | NIST |
ΔfH°liquid | [110.00; 110.60] | kJ/mol |
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ΔfH°liquid | 110.60 ± 1.80 | kJ/mol | NIST |
ΔfH°liquid | 110.00 ± 1.00 | kJ/mol | NIST |
ΔfusH° | 11.00 | kJ/mol | Joback Calculated Property |
ΔvapH° | 50.60 ± 1.50 | kJ/mol | NIST |
IE | [8.13; 8.62] | eV |
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IE | 8.14 ± 0.01 | eV | NIST |
IE | 8.33 ± 0.01 | eV | NIST |
IE | 8.14 ± 0.01 | eV | NIST |
IE | Outlier 8.62 | eV | NIST |
IE | 8.13 ± 0.05 | eV | NIST |
IE | 8.15 ± 0.01 | eV | NIST |
log10WS | -2.57 | Crippen Calculated Property | |
logPoct/wat | 2.256 | Crippen Calculated Property | |
McVol | 98.750 | ml/mol | McGowan Calculated Property |
Pc | 3800.00 | kPa | KDB |
Inp | [168.80; 1072.50] |
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|
Inp | 1059.00 | NIST | |
Inp | 1052.00 | NIST | |
Inp | 1059.00 | NIST | |
Inp | 1036.00 | NIST | |
Inp | 1015.00 | NIST | |
Inp | 1016.00 | NIST | |
Inp | 1034.00 | NIST | |
Inp | 1034.00 | NIST | |
Inp | 1031.00 | NIST | |
Inp | 1034.00 | NIST | |
Inp | 1031.00 | NIST | |
Inp | 1035.00 | NIST | |
Inp | 1026.00 | NIST | |
Inp | 1018.00 | NIST | |
Inp | 1013.00 | NIST | |
Inp | 1023.30 | NIST | |
Inp | 1059.00 | NIST | |
Inp | 1049.00 | NIST | |
Inp | 1059.00 | NIST | |
Inp | 1023.00 | NIST | |
Inp | 1011.80 | NIST | |
Inp | 1015.70 | NIST | |
Inp | 1034.10 | NIST | |
Inp | 1043.30 | NIST | |
Inp | 1053.80 | NIST | |
Inp | 1021.00 | NIST | |
Inp | 1011.80 | NIST | |
Inp | 1015.70 | NIST | |
Inp | 1016.90 | NIST | |
Inp | 1016.90 | NIST | |
Inp | 1017.00 | NIST | |
Inp | 1017.50 | NIST | |
Inp | 1060.00 | NIST | |
Inp | 1030.00 | NIST | |
Inp | 1062.00 | NIST | |
Inp | 1026.00 | NIST | |
Inp | 1037.00 | NIST | |
Inp | 1072.50 | NIST | |
Inp | 1069.00 | NIST | |
Inp | 1041.00 | NIST | |
Inp | 1045.00 | NIST | |
Inp | 1054.00 | NIST | |
Inp | 1011.00 | NIST | |
Inp | 1014.00 | NIST | |
Inp | 1036.00 | NIST | |
Inp | 1033.00 | NIST | |
Inp | 1051.00 | NIST | |
Inp | 1049.00 | NIST | |
Inp | 1039.00 | NIST | |
Inp | 1025.00 | NIST | |
Inp | 1024.00 | NIST | |
Inp | 1025.00 | NIST | |
Inp | 1042.00 | NIST | |
Inp | 1036.00 | NIST | |
Inp | 1060.00 | NIST | |
Inp | 1060.00 | NIST | |
Inp | 1041.00 | NIST | |
Inp | 1059.00 | NIST | |
Inp | 1031.00 | NIST | |
Inp | 1037.00 | NIST | |
Inp | 1020.00 | NIST | |
Inp | 1042.00 | NIST | |
Inp | 1045.00 | NIST | |
Inp | 1017.00 | NIST | |
Inp | 1059.00 | NIST | |
Inp | 1062.00 | NIST | |
Inp | Outlier 171.05 | NIST | |
Inp | Outlier 173.26 | NIST | |
Inp | Outlier 172.05 | NIST | |
Inp | Outlier 172.51 | NIST | |
Inp | Outlier 170.83 | NIST | |
Inp | Outlier 169.00 | NIST | |
Inp | Outlier 168.80 | NIST | |
Inp | Outlier 170.08 | NIST | |
Inp | Outlier 169.00 | NIST | |
Inp | Outlier 171.05 | NIST | |
Inp | 1060.00 | NIST | |
Inp | 1059.00 | NIST | |
Inp | 1016.00 | NIST | |
Inp | 1031.00 | NIST | |
Inp | 1023.30 | NIST | |
Inp | 1011.80 | NIST | |
Inp | 1021.00 | NIST | |
Inp | 1017.00 | NIST | |
I | [1430.80; 1479.00] |
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|
I | 1455.80 | NIST | |
I | 1430.80 | NIST | |
I | 1431.00 | NIST | |
I | 1471.00 | NIST | |
I | 1466.00 | NIST | |
I | 1472.00 | NIST | |
I | 1467.00 | NIST | |
I | 1479.00 | NIST | |
S°liquid | [214.18; 215.35] | J/mol×K |
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S°liquid | 214.18 | J/mol×K | NIST |
S°liquid | 215.35 | J/mol×K | NIST |
Tboil | 455.59 | K | KDB |
Tc | 695.15 | K | KDB |
Tfus | [270.48; 271.40] | K |
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Tfus | 271.00 | K | KDB |
Tfus | 271.40 ± 0.50 | K | NIST |
Tfus | 270.48 ± 0.30 | K | NIST |
Ttriple | 271.70 ± 0.02 | K | NIST |
Vc | 0.368 | m3/kmol | KDB |
Zc | 0.2422730 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [185.13; 249.87] | J/mol×K | [447.55; 677.06] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 180 190 200 210 220 230 240 250 500 600 | ||||
Cp,gas | 185.13 | J/mol×K | 447.55 | Joback Calculated Property |
Cp,gas | 198.30 | J/mol×K | 485.80 | Joback Calculated Property |
Cp,gas | 210.42 | J/mol×K | 524.05 | Joback Calculated Property |
Cp,gas | 221.55 | J/mol×K | 562.31 | Joback Calculated Property |
Cp,gas | 231.79 | J/mol×K | 600.56 | Joback Calculated Property |
Cp,gas | 241.21 | J/mol×K | 638.81 | Joback Calculated Property |
Cp,gas | 249.87 | J/mol×K | 677.06 | Joback Calculated Property |
Cp,liquid | [186.94; 186.94] | J/mol×K | [298.15; 298.15] | ![]() |
Cp,liquid | 186.94 | J/mol×K | 298.15 | NIST |
Cp,liquid | 186.94 | J/mol×K | 298.15 | NIST |
η | [0.0003712; 0.0014072] | Pa×s | [253.07; 447.55] | ![]() |
T(K) Dynamic viscosity (Pa×s) 4.00e-4 6.00e-4 8.00e-4 1.00e-3 1.20e-3 1.40e-3 300 400 | ||||
η | 0.0014072 | Pa×s | 253.07 | Joback Calculated Property |
η | 0.0009934 | Pa×s | 285.48 | Joback Calculated Property |
η | 0.0007529 | Pa×s | 317.90 | Joback Calculated Property |
η | 0.0006007 | Pa×s | 350.31 | Joback Calculated Property |
η | 0.0004979 | Pa×s | 382.72 | Joback Calculated Property |
η | 0.0004250 | Pa×s | 415.14 | Joback Calculated Property |
η | 0.0003712 | Pa×s | 447.55 | Joback Calculated Property |
ΔfusH | [10.20; 10.20] | kJ/mol | [271.70; 271.70] | ![]() |
ΔfusH | 10.20 | kJ/mol | 271.70 | NIST |
ΔfusH | 10.20 | kJ/mol | 271.70 | NIST |
ΔfusH | 10.20 | kJ/mol | 271.70 | NIST |
ΔvapH | [43.60; 45.30] | kJ/mol | [372.00; 413.00] | ![]() |
ΔvapH | 43.60 | kJ/mol | 372.00 | NIST |
ΔvapH | 43.90 | kJ/mol | 391.50 | NIST |
ΔvapH | 45.30 | kJ/mol | 413.00 | NIST |
n0 | 1.57370 | 298.15 | KDB | |
ρl | 998.99 | kg/m3 | 293.10 | KDB |
ΔfusS | 37.55 | J/mol×K | 271.70 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.64] | kPa | [335.62; 481.24] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.67872e+01 | |||
Coefficient B | -5.48854e+03 | |||
Coefficient C | -2.97000e+00 | |||
Temperature range, min. | 335.62 | |||
Temperature range, max. | 481.24 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400 450 | ||||
Pvap | 1.33 | kPa | 335.62 | Calculated Property |
Pvap | 2.87 | kPa | 351.80 | Calculated Property |
Pvap | 5.76 | kPa | 367.98 | Calculated Property |
Pvap | 10.90 | kPa | 384.16 | Calculated Property |
Pvap | 19.59 | kPa | 400.34 | Calculated Property |
Pvap | 33.63 | kPa | 416.52 | Calculated Property |
Pvap | 55.43 | kPa | 432.70 | Calculated Property |
Pvap | 88.11 | kPa | 448.88 | Calculated Property |
Pvap | 135.58 | kPa | 465.06 | Calculated Property |
Pvap | 202.64 | kPa | 481.24 | Calculated Property |
Pvap | [0.02; 4302.94] | kPa | [271.70; 693.15] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 1.22605e+02 | |||
Coefficient B | -1.05135e+04 | |||
Coefficient C | -1.58068e+01 | |||
Coefficient D | 9.00394e-06 | |||
Temperature range, min. | 271.70 | |||
Temperature range, max. | 693.15 | |||
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 400 600 | ||||
Pvap | 0.02 | kPa | 271.70 | Calculated Property |
Pvap | 0.55 | kPa | 318.53 | Calculated Property |
Pvap | 5.79 | kPa | 365.36 | Calculated Property |
Pvap | 31.43 | kPa | 412.18 | Calculated Property |
Pvap | 111.75 | kPa | 459.01 | Calculated Property |
Pvap | 301.25 | kPa | 505.84 | Calculated Property |
Pvap | 675.75 | kPa | 552.67 | Calculated Property |
Pvap | 1342.06 | kPa | 599.49 | Calculated Property |
Pvap | 2462.68 | kPa | 646.32 | Calculated Property |
Pvap | 4302.94 | kPa | 693.15 | Calculated Property |
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